CN106440545A - Refrigerant system, drying device and control method of refrigerant system - Google Patents
Refrigerant system, drying device and control method of refrigerant system Download PDFInfo
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Abstract
The invention discloses a refrigerant system which is used for a drying device. The refrigerant system comprises a condenser, an evaporator, a compressor, and a refrigerant line connected with the condenser, the evaporator and the compressor. The refrigerant system further comprises a flow control device arranged at the refrigerant line; a refrigerant inlet of the flow control device communicates with a refrigerant outlet of the condenser; the flow control device is provided with two refrigerant outlets that communicate with a refrigerant inlet of the evaporator and a refrigerant inlet of the compressor respectively; and the flow control device can adjust a refrigerant flow, and can switch on or off refrigerant circulation of a flow path between the refrigerant outlet of the condenser and the refrigerant inlet of the compressor. The refrigerant system can maintain a compressor exhaust temperature within an appropriate range and can reduce energy consumption. In addition, the invention also discloses the drying device applied to the refrigerant system, and a control method of the refrigerant system.
Description
Technical field
The present invention relates to dryer technical field, more particularly to a kind of drying unit, cold-producing medium
System and the control method of refrigerant system.
Background technology
Drying unit, such as heat pump clothes dryer, have the advantages that energy-saving and environmental protection and the suitability are wide,
It is increasingly becoming the development trend of dryer.
Heat pump clothes dryer makes medicated clothing heat up according to the condensation heat of cold-producing medium, and the moisture in medicated clothing becomes
For vapor, evaporation analysis moor reason is recycled so that vapor is separated out, thus realizing no aerofluxuss drying.
The refrigerant system of heat pump clothes dryer has air circulation system and refrigerant cycle is returned
Road.
Air circulation system includes hothouse, blower fan, condenser and vaporizer, this four parts
It is placed in airtight air duct, air circulation flow is driven by blower fan.The flow path of air
For：The air of high temperature drying from condenser out, enters hothouse, takes away medicated clothing in hothouse
Moisture, and by cooling become low temperature and high relative humidity air enter vaporizer；In vaporizer, air
With low-temperature refrigerant heat exchange, lowered the temperature further, because vaporizer wall surface temperature is less than dew point temperature
Degree, the hydrogenesis of in the air separate out for aqueous water；Vaporizer air out enters condenser,
Heated by high temperature refrigerant, again become the air of high temperature drying, enter back into hothouse, complete
Circulation.
Refrigerant circulation loop includes condenser, vaporizer, compressor and restricting element；Refrigeration
The flow path of agent is：The gaseous refrigerant compression of the low-temp low-pressure of compressor flash-pot in future
The cold-producing medium becoming High Temperature High Pressure is sent in condenser, is liquefied as the refrigeration of liquid by Cryogenic air
Agent is flowed out from condenser, is changed into two phase cold-producing mediums of low-temp low-pressure after restricting element, then
Enter vaporizer, enter into after being vaporized by high temperature air in compressor, complete to circulate.Wherein,
Restricting element has flow regulating function, can adjust the refrigerant flow entering vaporizer.
With the operation of refrigerant system, the delivery temperature of compressor understands more and more higher, thus empty
The heat of gas passage hollow aspiration gets more and more, and entering dry indoor air themperature can be more next
Higher, when temperature exceedes the limit temperature of medicated clothing, will result in laundry damage；In addition, mistake
High delivery temperature can affect the service life of compressor, and too high condensation temperature also can reduce pressure
The efficiency of contracting machine.
In order to avoid the generation of the problems referred to above, current common practice is to arrange separately at compressor
One blower fan, when delivery temperature compressor is detected is more than the upper limit of set point, just starting should
Blower fan is lowered the temperature to compressor, so the delivery temperature of compressor is limited in set point.
However, the energy that compressor work consuming produces is lost to environment by blower fan by this kind of mode
In, cause the waste of energy, particularly phase after the drying, medicated clothing moisture reduces, from air
The heat of middle absorption seldom, enters the pathogenic wind-warm more and more higher of vaporizer and condenser, corresponding system
The temperature of cryogen also more and more higher, in order to maintain stable compressor exhaust temperature, blower fan is opened
More frequent, the energy of waste is more.
In view of this, how on the basis of maintaining the suitable pathogenic wind-warm entering hothouse, reduce energy
Amount wastes, and is the current technical issues that need to address of those skilled in the art.
Content of the invention
It is an object of the invention to provide a kind of refrigerant system, for drying unit, this system energy
Enough maintain the compressor exhaust temperature of refrigerant system in OK range, reduce energy wave simultaneously
Take.On this basis, it is a further object of the present invention to provide a kind of this refrigerant system of application
Drying unit, and the control method of this refrigerant system.
For solving above-mentioned technical problem, the present invention provides a kind of refrigerant system, for drying dress
Put, including condenser, vaporizer, compressor and the described condenser of connection, described vaporizer
Refrigerant line with described compressor；
Also include the volume control device located at described refrigerant line, this volume control device
Refrigerant inlet is connected with the refrigerant outlet of described condenser, and this volume control device has two
Individual refrigerant outlet, two refrigerant outlets of this volume control device respectively with described vaporizer
Refrigerant inlet, described compressor refrigerant inlet connection；Described volume control device energy
Enough adjusting refrigerant flow rates, and can turn on or block described condenser refrigerant outlet with described
The cold-producing medium circulation of stream between compressor refrigerant entrance.
As above, this refrigerant system is additionally arranged a refrigerant line, and it can be by after partial throttling
Low-temperature refrigerant introduce the refrigerant inlet of compressor, this refrigerant line can pass through flow
The control of control device turns on or blocks；So, when the delivery temperature of compressor exceedes setting model
During the upper limit enclosed, turn on this refrigerant line, make the low-temperature refrigerant after partial throttling and warp
After the superheated refrigerant mixing of pervaporation device, then flow into compressor, thus reducing the suction of compressor
Temperature degree, and then reduce the delivery temperature of compressor, so that the delivery temperature of compressor is maintained and set
Determine in scope, indirectly maintain the inlet temperature of hothouse simultaneously in set point；With existing
Compared by the way of blower fan cooling compressor in technology, the program is passed through to reduce the suction of compressor
Temperature degree, to control its delivery temperature, thermal loss reduction, reduces energy dissipation.
Alternatively, described volume control device includes the first regulating valve and the second regulating valve；
Described first regulating valve, described second regulating valve refrigerant inlet all with described condenser
Refrigerant outlet connection；
The refrigerant outlet of described first regulating valve is connected with the refrigerant inlet of described vaporizer,
The refrigerant outlet of described second regulating valve is connected with the refrigerant inlet of described compressor.
Alternatively, described first regulating valve is electric expansion valve；Described second regulating valve is to have
Completely close the electric expansion valve of function or the electromagnetic valve that frequency is controlled, this electromagnetic valve according to opening,
The frequency adjusting refrigerant flow rate closing, during this closed electromagnetic valve, the cold-producing medium of its place stream is not led
Logical.
Alternatively, described first regulating valve is electric expansion valve；Described second regulating valve includes tool
There are the switch electromagnetic valve completely closing function and restricting element, described switch electromagnetic valve and described section
Fluid element is arranged in series.
Alternatively, described volume control device includes the first regulating valve being arranged in series and the second tune
Section valve；
The refrigerant inlet of described first regulating valve is connected with the refrigerant outlet of described condenser,
The refrigerant outlet of described first regulating valve respectively with the refrigerant inlet of described vaporizer, described
Second regulating valve refrigerant inlet connection, the refrigerant outlet of described second regulating valve with described
The refrigerant inlet connection of compressor.
Alternatively, described first regulating valve is electric expansion valve；Described second regulating valve is switch
Valve.
Alternatively, described switch valve is the controlled switch valve of aperture.
Alternatively, described refrigerant system is also associated with controller；
Described evaporator refrigerant outlet-side conduit is disposed with the first temperature sensor, described compression
Machine refrigerant outlet-side conduit is disposed with second temperature sensor；
Described evaporator refrigerant outlet-side conduit is disposed with pressure transducer, or, described steaming
Send out the coolant channel outer wall surface arrangement in the middle part of device refrigerant inlet lateral line or described vaporizer
There is three-temperature sensor；
The evaporator outlet temperature that described controller obtains according to described first temperature sensor detection
Degree and described pressure transducer detect that the evaporator exit pressure obtaining is calculated evaporator outlet
The current degree of superheat；Or, described controller obtains according to described first temperature sensor detection
Evaporator outlet temperature and the described three-temperature sensor evaporator temperature that obtains of detection
Or vaporizer middle portion temperature is calculated the current degree of superheat of evaporator outlet；
Described controller is according to the comparative result of the current degree of superheat and the degree of superheat threshold value setting, defeated
Go out control signal and control the aperture of described first regulating valve to adjust the refrigeration entering described vaporizer
Agent flux；
Described controller also judges the compressor air-discharging that described second temperature sensor detection obtains
Whether temperature is less than preset temperature, when detection temperature is less than preset temperature, closes described second tune
Section valve is to block stream between described condenser refrigerant outlet and described compressor refrigerant entrance
Cold-producing medium circulation；When detection temperature be not less than preset temperature, open described second regulating valve with
Turn on the refrigeration of stream between described condenser refrigerant outlet and described compressor refrigerant entrance
Agent is circulated.
Alternatively, the inlet and outlet of the hothouse of described drying unit is equipped with humidity sensor
Device；Described controller detects, according to two described humidity sensors, the air intake water capacity obtaining and goes out
Wind water capacity is calculated the degree of superheat threshold value of described setting.
The present invention also provides a kind of drying unit, including outer container, the drying in described outer container
Room and refrigerant system, also include the air duct connecting with described hothouse, described air
Passage is used for described hothouse input air, from described hothouse delivery air, described refrigeration
The condenser of agent system, vaporizer are located at described air duct；Described refrigerant system is above-mentioned
Refrigerant system described in any one；；Along the air-flow direction of described air duct, described steaming
Send out condenser described in device arm and be relatively distant from described hothouse, vaporizer phase described in described condenser arm
To near described hothouse.
The present invention also provides a kind of control method of refrigerant system, and described refrigerant system is upper
State the refrigerant system described in any one, described control method comprises the steps：
After drying starts, start compressor, described by controlling described volume control device to block
The cold-producing medium circulation of stream between condenser refrigerant outlet and described compressor refrigerant entrance；
Determine the setting degree of superheat threshold value of evaporator outlet；
Judge whether the current degree of superheat of evaporator outlet is not more than described setting degree of superheat threshold value,
When the current degree of superheat of evaporator outlet is not more than described setting degree of superheat threshold value, reduce to flow into and steam
Send out the refrigerant flow of device；When the current degree of superheat of evaporator outlet is more than the described setting degree of superheat
Threshold value, increases the refrigerant flow flowing into vaporizer；
Judge whether compressor exhaust temperature is not less than preset temperature, when compressor exhaust temperature is little
In preset temperature, block described condenser refrigerant outlet and described compressor refrigerant entrance it
Between stream cold-producing medium circulation；When compressor exhaust temperature is not less than preset temperature, conducting is described
The cold-producing medium circulation of stream between condenser refrigerant outlet and described compressor refrigerant entrance.
Alternatively, detect air intake humidity and the air-out humidity of hothouse by humidity sensor, obtain
Take the water capacity of hothouse air inlet/outlet poor, evaporator outlet is calculated according to described water capacity difference
Setting degree of superheat threshold value.
Brief description
Fig. 1 is that the principle of the first embodiment of the refrigerant system of dryer provided by the present invention is shown
It is intended to；
Fig. 2 is the structural representation of refrigerant system shown in Fig. 1；
Fig. 3 is the upward view of refrigerant system shown in Fig. 2；
Fig. 4 is that the principle of the second embodiment of the refrigerant system of dryer provided by the present invention is shown
It is intended to；
Fig. 5 is the schematic flow sheet of the control method providing refrigerant system of the present invention.
Wherein, in Fig. 1 to Fig. 4, the one-to-one relationship between component names and reference is such as
Shown in lower：
Hothouse 10, air duct 11, blower fan 12；
Condenser 20, vaporizer 30, compressor 40, the first electric expansion valve 50, the second electricity
Sub- expansion valve 60, switch valve 60 ', the first temperature sensor 70a, second temperature sensor 70b.
Specific embodiment
The core of the present invention is to provide a kind of refrigerant system, for drying unit, this system energy
Enough maintain the compressor exhaust temperature of refrigerant system in OK range, reduce energy wave simultaneously
Take.On this basis, it is a further object of the present invention to provide a kind of this refrigerant system of application
Drying unit, and the control method of this refrigerant system.
Without loss of generality, with heat pump clothes dryer and its refrigerant system, control method it is herein
Example illustrates, and specifically, this refrigerant system is heat pump.
In order that those skilled in the art more fully understand the present invention program, below in conjunction with the accompanying drawings
The present invention is described in further detail with specific embodiment.
Refer to shown in Fig. 1-3, Fig. 1 is the principle of the first embodiment of described refrigerant system
Schematic diagram；Fig. 2 is the structural representation of refrigerant system shown in Fig. 1；Fig. 3 is facing upward of Fig. 2
View.
In this embodiment, the refrigerant system of heat pump clothes dryer has air circulation system and system
Refrigerant cycle loop.
Described refrigerant circulation loop includes condenser 20, vaporizer 30, compressor 40 and stream
Amount control device；The refrigerant outlet of vaporizer 30 connects the refrigerant inlet of compressor 40,
The refrigerant outlet of compressor 40 connects the refrigerant inlet of condenser 20；The system of condenser 20
Cryogen outlet had both connected the refrigerant outlet of vaporizer 30, connected the cold-producing medium of compressor 40 again
Outlet." connect " in this specification include by pipeline and/or other connectors directly connection or
Indirect communication, and be not limited to each element and connection is realized by pipeline.
In a kind of air circulation mode that hollow arrow in Fig. 1, Fig. 3 is illustrated as a example, wherein,
Described air circulation system includes air duct 11, the wind connecting with the space in hothouse 10
Machine 12, this blower fan 12, condenser 20 and vaporizer 30 are located in air duct 11.Wherein,
Air duct 11 is used for, to hothouse 10 input air, from hothouse 10 delivery air, condensing
Device 20, vaporizer 30 are located at this air duct 11, along the air-flow direction of air duct 11,
Vaporizer 30 is relatively distant from hothouse 10 than condenser 20, and condenser 20 is than vaporizer 30 phase
The air near hothouse 10, flowing out from hothouse 10 is first passed through vaporizer 30 dehumidify,
Again after condenser 20 heat temperature raising, enter back into hothouse 10.Blower fan 12 is arranged on drying
The upstream (on the basis of air-flow direction) of room 10, this blower fan 12 is used for driving air in sky
Flow through hothouse 10, vaporizer 30, condenser 20 in gas passage 11 successively, enter back into drying
Room 10, forms air circulation loop；Described in other embodiment, air circulation system is alternatively
The air inlet of open in line air circulation system, such as air circulation system communicated with indoor environment,
Exhaust outlet is communicated with outdoor environment, with realize from indoor suction air, through hothouse heat exchange again
To outdoor discharge gas.
Cold-producing medium between described condenser 20 refrigerant outlet and vaporizer 30 refrigerant inlet
First regulating valve is arranged on pipeline, this restricting element is used for adjusting refrigerant flow rate size, this reality
Apply and in scheme, be specifically set to the first electric expansion valve 50；Described condenser 20 refrigerant outlet with
Second regulating valve, the second regulation are arranged on the refrigerant line between compressor 40 refrigerant inlet
Valve is disposed in parallel two branch road, in the present embodiment, institute with aforementioned first regulating valve
State the part that the second regulating valve is that restricting element and switch valve integrate, can turn on, block
The cold-producing medium circulation of stream between condenser 20 refrigerant outlet and compressor 40 refrigerant inlet,
And adjusting refrigerant flow rate size, specifically may be configured as that there is the second electricity completely closing function
Sub- expansion valve 60；Certainly, in other embodiments, described second regulating valve could be arranged to be had
Have the controlled electromagnetic valve of the frequency completely closing function, this electromagnetic valve according to the frequency of open and close Lai
Adjustment refrigerant flow, during this closed electromagnetic valve, the cold-producing medium of its place stream is not turned on；In addition,
Also the controlled electromagnetic valve of said frequencies can be replaced with switch valve by the restricting element being arranged in series,
Can turn on, block stream between condenser 20 refrigerant outlet and compressor 40 refrigerant inlet
The cold-producing medium circulation on road, and adjusting refrigerant flow rate size, specifically, restricting element
Capillary tube can be set to, switch valve can be set to the electromagnetic valve with on-off function.
As shown in figure 1, described volume control device includes the first electric expansion valve 50 and second
Electric expansion valve 60, both are both connected on condenser 20 refrigerant outlet pipeline.
So, in this embodiment, the flow path of cold-producing medium is：Compressor 40 will be from steaming
The gaseous refrigerant sending out the low-temp low-pressure of device 30 is compressed into the gaseous refrigerant feeding of High Temperature High Pressure
Condenser 20, is cooled down by the air of relative low temperature, flows out and become room temperature height from condenser 20
Hydraulic fluid cryogen, simultaneously air side be heated up；When the second electric expansion valve 60 is closed,
Refrigerant line between condenser 20 refrigerant outlet and compressor 40 refrigerant inlet is cut
Only, the cold-producing medium flowing out in condenser 20 flows into vaporizer 30 through the first electric expansion valve 50,
When the second electric expansion valve 60 is opened, condenser 20 refrigerant outlet and compressor 40 cold-producing medium
Refrigerant line between entrance is switched on, and the cold-producing medium part flowing out in condenser 20 is through the
One electric expansion valve 50 flows into vaporizer 30, separately has minimal amount cold-producing medium (according to actual needs
Determine concrete flow) after the second electric expansion valve 60 reducing pressure by regulating flow, it is changed into the gas of low-temp low-pressure
Liquid two phase cold-producing medium；It is low that cold-producing medium in entrance vaporizer 30 is vaporizated into low temperature by high temperature air
The gaseous refrigerant of pressure, flows through a small amount of low-temperature refrigerant of the second electric expansion valve 60 and flows through steaming
Send out device 30 overheated gaseous refrigerant converge after, formed low-temp low-pressure gaseous refrigerant (still have
Have the higher degree of superheat) enter compressor 40.Refrigeration is represented with filled arrows in Fig. 1 and Fig. 3
The flow path of agent.
As above, compared with prior art, the refrigerant system setting refrigerant pipe in this embodiment
Road branch, i.e. refrigeration between condenser 20 refrigerant outlet and compressor 40 refrigerant inlet
Agent pipeline, in this refrigerant line branch, the second electric expansion valve 60 of setting has throttling and leads to
Disconnected function, the low-temperature refrigerant that can form the cold-producing medium that condenser 20 flows out after throttling draws
Enter the refrigerant inlet of compressor 40；So, when the excessive discharge temperature of compressor 40, surpass
Cross set point the upper limit when, open the second electric expansion valve 60, make the low temperature after partial throttling
Cold-producing medium is converged with the relatively warm refrigerant through vaporizer 30, flows into compressor 40 together, thus
Reduce the suction temperature of compressor 40, and then reduce the delivery temperature of compressor 40, can
So that the delivery temperature of compressor 40 is maintained in set point, prevent compressor 40 delivery temperature
Too high impact service life, system heat exchange efficiency are low, meanwhile, air to refrigerant side heat exchange
For side, the inlet temperature of hothouse 10 can be prevented too high, evade and causing because drying temperature is too high
Laundry damage；In addition, when inlet temperature is low, this refrigerant line branch can be blocked,
To improve the heat exchange efficiency of refrigerant system.
Compared with prior art using blower fan cooling compressor, the program is drawn in suction port of compressor
Enter the low-temperature refrigerant after partial throttling, compression is maintained by the suction temperature reducing compressor
The delivery temperature of machine and the inlet temperature of hothouse, thermal loss reduces, and reduces energy dissipation.
Further, described refrigerant system also includes controller, and this controller can control first
The aperture (or hydrojet frequency) of the aperture of electric expansion valve 50 and the second electric expansion valve 60 and
Break-make.
Specifically, it is provided with the first temperature sensor 70a and pressure transducer in vaporizer 30 outlet
(not shown), for detecting vaporizer 30 outlet temperature and outlet pressure, this vaporizer
30 outlet temperatures are the actual temperature of evaporator outlet side cold-producing medium.Described controller is according to collection
To vaporizer 30 outlet temperature and outlet pressure can be calculated vaporizer 30 outlet current
The degree of superheat.Described controller, according to the current degree of superheat of vaporizer 30, adjusts the first electronic expansion
The aperture of valve 50, to control the refrigerant flow entering vaporizer 30, makes vaporizer 30 export
As far as possible near but less than set degree of superheat threshold value.
Wherein, the degree of superheat threshold value of described setting can be contained by detecting the import and export of hothouse 10
Moisture calculates.Specifically, the import and export in hothouse 10 are respectively provided with humidity sensor (figure
Not shown in), for detecting air intake humidity and the air-out humidity of hothouse 10, described controller
The detection of humidity sensor according to two is worth to the air-out humidity of hothouse 10 and enters rheumatism
The water capacity difference △ d of degree, can be calculated degree of superheat threshold value accordingly, as aforementioned setting overheated
Degree threshold value.
This degree of superheat threshold value can be represented with formula S Hmax=a-b* △ d, and wherein, a, b meet
Inverse ratio linear relationship, that is, described water capacity difference is less, and degree of superheat threshold value is bigger；For example before drying
If phase degree of superheat threshold value is set as 5 DEG C, drying later stage water capacity subtractive is little, and degree of superheat threshold value can
Reach 15～25 DEG C.
The degree of superheat threshold value of the setting of described vaporizer 30 outlet is according to hothouse 10 containing wet journey
Spend and to set, the different phase in dry run, such as dry early stage, dry mid-term and drying
In the later stage, water capacity is exported by above-mentioned hothouse 10, different phase, hothouse are being dried
The moisture content of 10 undergarments is different, and the ability absorbing heat is also corresponding different, by above method,
The setting that adjustment vaporizer 30 exports can be corresponded to according to the moisture content of hothouse 10 undergarment
Degree of superheat threshold value, can make refrigerant system maintain power corresponding with drying regime and heat exchange amount,
Reduce energy dissipation.
Specifically, described controller compares the current degree of superheat and the setting of vaporizer 30 outlet
Degree of superheat threshold value, if the current degree of superheat is not more than the degree of superheat threshold value setting, reduces the first electricity
The aperture of sub- expansion valve 50, that is, reduce refrigerant flow, enough to ensure drying temperature；If working as
The front degree of superheat is more than the degree of superheat threshold value setting, then increase the aperture of the first electric expansion valve 50,
Increase refrigerant flow, lift system heat exchange amount.
Described controller is also stored with compressor air-discharging preset temperature, and this compressor air-discharging presets temperature
Degree can set according to the actual requirements；Compressor 40 refrigerant outlet lateral line is disposed with the second temperature
Degree sensor 70b, for detecting the delivery temperature of compressor 40 outlet；Described controller is also sentenced
The compressor exhaust temperature of disconnected second temperature sensor 70b detection is less than the pre- of compressor 40 aerofluxuss
If during temperature, close the second electric expansion valve 60；And judge that second temperature sensor 70b detects
Compressor exhaust temperature be not less than compressor 40 aerofluxuss preset temperature when, open the second electronics
Expansion valve 60, and continue for some time, until compressor 40 delivery temperature is less than preset temperature,
Turn off the second electric expansion valve 60.
Further, it is also possible to obtain the current degree of superheat of vaporizer 30 outlet by other means.
Specifically, vaporizer 30 exports and still arranges the first temperature sensor 70a, for detecting vaporizer
30 outlet temperatures, separately outer wall surface setting the 3rd in the middle part of vaporizer 30 import or vaporizer 30
Temperature sensor, for detecting vaporizer 30 inlet temperature or middle portion temperature；Described controller root
Calculate according to vaporizer 30 outlet temperature collecting and vaporizer 30 inlet temperature or middle portion temperature
Obtain the current degree of superheat of vaporizer 30 outlet.
Refer to Fig. 4, Fig. 4 is the second reality of the refrigerant system of dryer provided by the present invention
Apply the principle schematic of example.
This embodiment is with the component that first embodiment function communicates or structure in the diagram with identical mark
Remember rower into show, to express the difference between two schemes further and to contact.
In this embodiment, the air circulation system of refrigerant system and aforementioned first embodiment one
Cause, be not repeated to discuss herein.
In this embodiment, in the refrigerant circulation loop of refrigerant system, condenser 20 with steam
Send out on refrigerant line between device 30 and compressor 40 volume control device of setting with aforementioned
First embodiment is different.
As shown in figure 4, being provided with the first regulating valve on the refrigerant outlet pipeline of condenser 20,
The outlet of this first regulating valve separates two branch roads, is respectively communicated with the refrigerant inlet of vaporizer 30
Refrigerant inlet with compressor 40；Wherein, this first regulating valve has flow regulating function,
And, it is provided with the second regulating valve between this first regulating valve and refrigerant inlet of compressor 40.
It is separately positioned on condenser with respect to the first regulating valve in aforementioned first embodiment and the second regulating valve
Two branch roads being arranged in parallel of 20 export pipelines, in this embodiment, the first regulating valve is adjusted with second
Section valve can be regarded as being arranged in series.
In the program, described first regulating valve is specially the first electric expansion valve 50.
Because the cold-producing medium of condenser 20 outflow is first through the first electric expansion valve 50, inborn ability afterwards
Stream flows into compressor 40, so, the second regulating valve herein can only have on-off function, that is,
Switch valve 60 ', such as has the electromagnetic valve of on-off function, certainly, is set to have and closes completely
The electric expansion valve closing function is also feasible.Further, switch valve 60 ' can be set to aperture
Controlled switch valve.
In this embodiment, the flow path of cold-producing medium is：Compressor flash-pot in 40 future 30
Low-temp low-pressure gaseous refrigerant be compressed into High Temperature High Pressure cold-producing medium send into condenser 20 in,
The cold-producing medium that liquid is liquefied as by Cryogenic air flow out from condenser 20 after through the first electronics
Expansion valve 50 throttles and controls flow；When switch valve 60 ' cuts out, the first electric expansion valve 50
Refrigerant line to compressor 40 refrigerant inlet is cut off, and the cold-producing medium after throttling is only
Flow into vaporizer 30, when switch valve 60 ' is opened, electric expansion valve 50 freezes to compressor 40
The refrigerant line of agent entrance is switched on, and the cold-producing medium part after throttling flows into vaporizer 30,
Another part flows into compressor 40 through switch valve 60 '；The cold-producing medium entering in vaporizer 30 is high
Compressor 40 is entered back into after warm air vaporization.
Obviously, identical with first embodiment principle, in this embodiment, it is also to be additionally arranged one to incite somebody to action
Low-temperature refrigerant after throttling introduces the refrigerant inlet lateral line of compressor 40, similarly, when
During compressor 40 excessive discharge temperature, switch valve 60 ' can be opened, make the low temperature after partial throttling
The superheated refrigerant that cold-producing medium is flowed out with vaporizer 30 flows into compressor 40 after mixing, to reduce
The intake air temperature of compressor 40, maintains the delivery temperature of compressor 40 and the air intake of hothouse 10
Temperature is in set point.
Correspondingly, for controlling the aperture of the first electric expansion valve 50 and the break-make of switch valve 60 ' etc.,
It is also equipped with controller and corresponding sensor, concrete setting is real with aforementioned first in this embodiment
Apply example to be similar to.Here repeat no more.
The present invention also provides a kind of drying unit, such as heat pump clothes dryer, including outer container, drying
Room and the refrigerant system in described outer container, for drying medicated clothing, described refrigerant system
For refrigerant system described above.
Because above-mentioned refrigerant system has above-mentioned technique effect, so applying this refrigerant system
Heat pump clothes dryer also there is corresponding technique effect, repeat no more here.
The present invention also provides a kind of control method of the refrigerant system based on aforementioned drying unit,
With reference to Fig. 5, this control method comprises the steps：
S11, drying are initial, and closing the second regulating valve (for first embodiment, second
Regulating valve is the second electric expansion valve 60, and for second embodiment, the second regulating valve is to open
Close valve 60 ', open the first regulating valve (for first embodiment and second embodiment, the first regulation
Valve is the first electric expansion valve 50)；Start hothouse motor, blower fan and compressor successively；
The early stage of drying, medicated clothing moisture content is high, and the delivery temperature of compressor is relatively low, now, need not
Reduce the delivery temperature of compressor, so when drying is initial, the second regulating valve is in closing shape
State.
S12, to judge that whether the air inlet/outlet water capacity difference of hothouse is not more than default water capacity poor,
It is to enter step S20；No, enter step S13；
Medicated clothing moisture content is poor corresponding with hothouse air inlet/outlet water capacity, and that is, hothouse air inlet/outlet is containing wet
When amount difference is larger, the moisture content of medicated clothing is higher, shows to be in the early stage of drying, hothouse air inlet/outlet
When water capacity is less, the moisture content of medicated clothing is relatively low, shows to be in the later stage of drying；When hothouse enters
Air-out water capacity difference is less than during certain value it is believed that drying terminates, it is to avoid over-drying damage clothing
Thing.
Described default water capacity difference can set according to the actual requirements.
S13, determine that the setting of evaporator outlet is overheated according to the air inlet/outlet water capacity of hothouse difference
Degree threshold value；
S14, judge that whether the current degree of superheat of evaporator outlet is not more than the described setting degree of superheat
Threshold value, is to reduce the aperture of the first regulating valve, no, increases the aperture of the first regulating valve；
S15, judge that whether compressor exhaust temperature is not less than default temperature range, be to beat
Open the second regulating valve, no, close the second regulating valve；
Return again to step 12；
Compressor exhaust temperature obtains according to the second temperature sensor located at compressor outlet.
Mid-term is dried, is gradually lowered with medicated clothing moisture content, absorption heat is more and more slower, compression
The delivery temperature of machine also corresponding more and more higher, is higher than default when compressor exhaust temperature is detected
During temperature range, that is, open the second regulating valve, make the part cryogenic refrigeration through throttling after condenser
Agent is mixed with the superheat refrigeration device through vaporizer, to reduce the suction temperature of compressor, thus
Reduce the delivery temperature of compressor；When the delivery temperature of compressor decreases below default temperature
During scope, close the second regulating valve.
The later stage of drying, medicated clothing absorbs the ability considerable decrease of heat, is contained according to hothouse air inlet/outlet
Moisture can improve the setting degree of superheat threshold value of evaporator outlet, reduces the aperture of the first regulating valve,
Reduce refrigerant flow, make refrigerant system maintain less power and heat exchange amount, reduce energy
Waste.
Step 20, successively close compressor, blower fan and hothouse motor, drying terminates.
Control to drying unit provided by the present invention, refrigerant system and refrigerant system above
Method processed is all described in detail.Specific case used herein to the principle of the present invention and
Embodiment is set forth, and the explanation of above example is only intended to help understand the present invention's
Method and its core concept.It should be pointed out that for those skilled in the art,
Under the premise without departing from the principles of the invention, the present invention can also be carried out with some improvement and modify,
These improve and modify and also fall in the protection domain of the claims in the present invention.
Claims (12)
1. a kind of refrigerant system, for drying unit, including condenser, vaporizer, pressure
Contracting machine and the refrigerant line connecting described condenser, described vaporizer and described compressor；
It is characterized in that：
Also include the volume control device located at described refrigerant line, this volume control device
Refrigerant inlet is connected with the refrigerant outlet of described condenser, and this volume control device has two
Individual refrigerant outlet, two refrigerant outlets of this volume control device respectively with described vaporizer
Refrigerant inlet, described compressor refrigerant inlet connection；Described volume control device energy
Enough adjusting refrigerant flow rates, and can turn on or block described condenser refrigerant outlet with described
The cold-producing medium circulation of stream between compressor refrigerant entrance.
2. refrigerant system according to claim 1 it is characterised in that：
Described volume control device includes the first regulating valve and the second regulating valve；
Described first regulating valve, described second regulating valve refrigerant inlet all with described condenser
Refrigerant outlet connection；
The refrigerant outlet of described first regulating valve is connected with the refrigerant inlet of described vaporizer,
The refrigerant outlet of described second regulating valve is connected with the refrigerant inlet of described compressor.
3. refrigerant system according to claim 2 it is characterised in that：
Described first regulating valve is electric expansion valve；Described second regulating valve is to have to completely close
The electric expansion valve of function or the controlled electromagnetic valve of frequency, this electromagnetic valve is according to the frequency of open and close
Rate adjusting refrigerant flow rate, during this closed electromagnetic valve, the cold-producing medium of its place stream is not turned on.
4. refrigerant system according to claim 2 is it is characterised in that described first
Regulating valve is electric expansion valve；Described second regulating valve includes thering is the switch completely closing function
Electromagnetic valve and restricting element, described switch electromagnetic valve is arranged in series with described restricting element.
5. refrigerant system according to claim 1 it is characterised in that：
Described volume control device includes the first regulating valve being arranged in series and the second regulating valve；
The refrigerant inlet of described first regulating valve is connected with the refrigerant outlet of described condenser,
The refrigerant outlet of described first regulating valve respectively with the refrigerant inlet of described vaporizer, described
Second regulating valve refrigerant inlet connection, the refrigerant outlet of described second regulating valve with described
The refrigerant inlet connection of compressor.
6. refrigerant system according to claim 5 it is characterised in that：
Described first regulating valve is electric expansion valve；Described second regulating valve is switch valve.
7. refrigerant system according to claim 6 is it is characterised in that described switch
Valve is the controlled switch valve of aperture.
8. the refrigerant system according to any one of claim 2-7 is it is characterised in that institute
State refrigerant system and be also associated with controller；
Described evaporator refrigerant outlet-side conduit is disposed with the first temperature sensor, described compression
Machine refrigerant outlet-side conduit is disposed with second temperature sensor；
Described evaporator refrigerant outlet-side conduit is disposed with pressure transducer, or, described steaming
Send out the coolant channel outer wall surface arrangement in the middle part of device refrigerant inlet lateral line or described vaporizer
There is three-temperature sensor；
The evaporator outlet temperature that described controller obtains according to described first temperature sensor detection
Degree and described pressure transducer detect that the evaporator exit pressure obtaining is calculated evaporator outlet
The current degree of superheat；Or, described controller obtains according to described first temperature sensor detection
Evaporator outlet temperature and the described three-temperature sensor evaporator temperature that obtains of detection
Or vaporizer middle portion temperature is calculated the current degree of superheat of evaporator outlet；
Described controller is according to the comparative result of the current degree of superheat and the degree of superheat threshold value setting, defeated
Go out control signal and control the aperture of described first regulating valve to adjust the refrigeration entering described vaporizer
Agent flux；
Described controller also judges the compressor air-discharging that described second temperature sensor detection obtains
Whether temperature is less than preset temperature, when detection temperature is less than preset temperature, closes described second tune
Section valve is to block stream between described condenser refrigerant outlet and described compressor refrigerant entrance
Cold-producing medium circulation；When detection temperature be not less than preset temperature, open described second regulating valve with
Turn on the refrigeration of stream between described condenser refrigerant outlet and described compressor refrigerant entrance
Agent is circulated.
9. refrigerant system according to claim 8 is it is characterised in that described drying
The inlet and outlet of the hothouse of device is equipped with humidity sensor；Described controller is according to two
Air intake water capacity that the detection of described humidity sensor obtains and air-out water capacity set described in being calculated
Fixed degree of superheat threshold value.
10. a kind of drying unit, including outer container, the hothouse in described outer container and system
Cryogen system, also includes the air duct connecting with described hothouse, and described air duct is used for
To described hothouse input air, from described hothouse delivery air, described refrigerant system
Condenser, vaporizer are located at described air duct；Described refrigerant system is claim 1-9
Refrigerant system described in any one；Along the air-flow direction of described air duct, described steaming
Send out condenser described in device arm and be relatively distant from described hothouse, vaporizer phase described in described condenser arm
To near described hothouse.
A kind of 11. control methods of refrigerant system, described refrigerant system is claim 1-9
Refrigerant system described in any one, described control method comprises the steps：
After drying starts, start compressor, described by controlling described volume control device to block
The cold-producing medium circulation of stream between condenser refrigerant outlet and described compressor refrigerant entrance；
Determine the setting degree of superheat threshold value of evaporator outlet；
Judge whether the current degree of superheat of evaporator outlet is not more than described setting degree of superheat threshold value,
When the current degree of superheat of evaporator outlet is not more than described setting degree of superheat threshold value, reduce to flow into and steam
Send out the refrigerant flow of device；When the current degree of superheat of evaporator outlet is more than the described setting degree of superheat
Threshold value, increases the refrigerant flow flowing into vaporizer；
Judge whether compressor exhaust temperature is not less than preset temperature, when compressor exhaust temperature is little
In preset temperature, block described condenser refrigerant outlet and described compressor refrigerant entrance it
Between stream cold-producing medium circulation；When compressor exhaust temperature is not less than preset temperature, conducting is described
The cold-producing medium circulation of stream between condenser refrigerant outlet and described compressor refrigerant entrance.
12. control methods according to claim 9 are it is characterised in that pass through humidity sensor
The air intake humidity of detection hothouse and air-out humidity, the water capacity obtaining hothouse air inlet/outlet is poor,
It is calculated the setting degree of superheat threshold value of evaporator outlet according to described water capacity difference.
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107444420A (en) * | 2017-08-07 | 2017-12-08 | 中车青岛四方车辆研究所有限公司 | Track vehicle air conditioner and its constant temperature dehumidification method |
| CN107841863A (en) * | 2017-10-17 | 2018-03-27 | 广东美的制冷设备有限公司 | Drying control method, drying control device, dehumidifier and readable storage medium storing program for executing |
| CN111201411A (en) * | 2017-10-12 | 2020-05-26 | 大金工业株式会社 | Refrigerating device |
| CN114303032A (en) * | 2019-10-29 | 2022-04-08 | 大金工业株式会社 | Refrigerant system |
| WO2023179232A1 (en) * | 2022-03-23 | 2023-09-28 | 宁德时代新能源科技股份有限公司 | Temperature management device and test system |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005075728A1 (en) * | 2004-02-04 | 2005-08-18 | Matsushita Electric Industrial Co., Ltd. | Drying apparatus and operating method thereof |
| CN1906451A (en) * | 2004-04-09 | 2007-01-31 | 松下电器产业株式会社 | Drying equipment |
| EP2489775A1 (en) * | 2011-02-18 | 2012-08-22 | Electrolux Home Products Corporation N.V. | A heat pump laundry dryer and a method for operating a heat pump laundry dryer |
| EP2527522A1 (en) * | 2011-05-26 | 2012-11-28 | Electrolux Home Products Corporation N.V. | A heat pump laundry dryer |
| CN103392036A (en) * | 2011-02-18 | 2013-11-13 | 伊莱克斯家用产品股份有限公司 | A heat pump laundry dryer |
| CN203295854U (en) * | 2013-01-22 | 2013-11-20 | 秦海涛 | Clothes drying system based on CO2 trans-critical heat pump circulating system |
| CN104005214A (en) * | 2013-02-22 | 2014-08-27 | 海尔集团公司 | Control method of heat pump clothes dryer expansion valve |
| JP2014204883A (en) * | 2013-04-15 | 2014-10-30 | 株式会社東芝 | Heat pump drying machine |
| CN104695193A (en) * | 2015-02-12 | 2015-06-10 | 珠海格力电器股份有限公司 | Heat pump clothes dryer and control method thereof |
-
2015
- 2015-08-10 CN CN201510487215.5A patent/CN106440545A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005075728A1 (en) * | 2004-02-04 | 2005-08-18 | Matsushita Electric Industrial Co., Ltd. | Drying apparatus and operating method thereof |
| CN1906451A (en) * | 2004-04-09 | 2007-01-31 | 松下电器产业株式会社 | Drying equipment |
| EP2489775A1 (en) * | 2011-02-18 | 2012-08-22 | Electrolux Home Products Corporation N.V. | A heat pump laundry dryer and a method for operating a heat pump laundry dryer |
| CN103392036A (en) * | 2011-02-18 | 2013-11-13 | 伊莱克斯家用产品股份有限公司 | A heat pump laundry dryer |
| EP2527522A1 (en) * | 2011-05-26 | 2012-11-28 | Electrolux Home Products Corporation N.V. | A heat pump laundry dryer |
| CN203295854U (en) * | 2013-01-22 | 2013-11-20 | 秦海涛 | Clothes drying system based on CO2 trans-critical heat pump circulating system |
| CN104005214A (en) * | 2013-02-22 | 2014-08-27 | 海尔集团公司 | Control method of heat pump clothes dryer expansion valve |
| JP2014204883A (en) * | 2013-04-15 | 2014-10-30 | 株式会社東芝 | Heat pump drying machine |
| CN104695193A (en) * | 2015-02-12 | 2015-06-10 | 珠海格力电器股份有限公司 | Heat pump clothes dryer and control method thereof |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107444420A (en) * | 2017-08-07 | 2017-12-08 | 中车青岛四方车辆研究所有限公司 | Track vehicle air conditioner and its constant temperature dehumidification method |
| CN111201411A (en) * | 2017-10-12 | 2020-05-26 | 大金工业株式会社 | Refrigerating device |
| CN111201411B (en) * | 2017-10-12 | 2021-11-30 | 大金工业株式会社 | Refrigerating device |
| US11415345B2 (en) | 2017-10-12 | 2022-08-16 | Daikin Industries, Ltd. | Refrigeration apparatus |
| CN107841863A (en) * | 2017-10-17 | 2018-03-27 | 广东美的制冷设备有限公司 | Drying control method, drying control device, dehumidifier and readable storage medium storing program for executing |
| CN107841863B (en) * | 2017-10-17 | 2020-06-19 | 广东美的制冷设备有限公司 | Clothes drying control method, clothes drying control device, dehumidifier and readable storage medium |
| CN114303032A (en) * | 2019-10-29 | 2022-04-08 | 大金工业株式会社 | Refrigerant system |
| WO2023179232A1 (en) * | 2022-03-23 | 2023-09-28 | 宁德时代新能源科技股份有限公司 | Temperature management device and test system |
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Application publication date: 20170222 |